Method for treating high-ammonia-nitrogen wastewater by feeding polyurethane filler
A technology of polyurethane filler and high ammonia nitrogen, which is applied in aerobic process treatment, anaerobic digestion treatment, chemical instruments and methods, etc., can solve problems such as secondary pollution, affecting the operation of biochemical systems, and affecting coal chemical enterprises, etc., to increase the load ability and impact resistance, increase sludge concentration and stability, and achieve harmless and resourceful effects
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Embodiment 1
[0042] Take high ammonia nitrogen wastewater, the ammonia nitrogen content is 3000mg / L, and the COD concentration is 600mg / L.
[0043] Add sodium hydroxide to the high ammonia nitrogen wastewater, adjust the pH to 10.5, enter the airtight reaction column for aeration, the aeration rate is 100L / L / h (air / water / hour), the aeration time is 90min, and the gas outlet uses acid The separated ammonia gas is recovered and reused, and the concentration of ammonia nitrogen in the waste water is 300mg / L after blowing off the nitrogen.
[0044] Add hydrochloric acid to the wastewater after blowing off nitrogen to adjust the pH to neutral, add sodium bicarbonate to adjust the alkalinity to 2000, enter the aerobic tank for full aeration, fill the aerobic tank with 30% polyurethane filler, and stay for 20 hours.
[0045] The effluent of the aerobic tank was added with 500mg / L glucose as an additional carbon source, and entered into the anoxic tank for reaction, and the anoxic tank was filled ...
Embodiment 2
[0048] Take high ammonia nitrogen wastewater, the ammonia nitrogen content is 3200mg / L, and the COD concentration is 550mg / L.
[0049]Add potassium hydroxide to the high ammonia nitrogen wastewater, adjust the pH to 11, enter the airtight reaction column for aeration, the aeration rate is 120L / L / h (air / water / hour), the aeration time is 70min, and the air outlet uses acid The separated ammonia gas is recovered and reused, and the concentration of ammonia nitrogen in the waste water is 320 mg / L after blowing off the nitrogen.
[0050] Add hydrochloric acid to the wastewater after nitrogen removal to adjust the pH to neutral, add sodium bicarbonate to adjust the alkalinity to 2400, enter the aerobic tank for full aeration, fill the aerobic tank with 30% polyurethane filler, and stay for 15 hours.
[0051] Add 600mg / L of sodium acetate as an external carbon source to the effluent of the aerobic tank, and enter the anoxic tank for reaction. The anoxic tank is filled with 50% polyur...
Embodiment 3
[0054] Take high ammonia nitrogen wastewater with an ammonia nitrogen content of 3500mg / L and a COD concentration of 700mg / L.
[0055] Add sodium hydroxide to the high ammonia nitrogen wastewater, adjust the pH to 10.8, enter the airtight reaction column for aeration, the aeration rate is 110L / L / h (air / water / hour), the aeration time is 60min, and the air outlet uses acid The separated ammonia gas is recovered and reused, and the concentration of ammonia nitrogen in the waste water is 340mg / L after the nitrogen is blown off.
[0056] Add hydrochloric acid to the wastewater after blowing off nitrogen to adjust the pH to neutral, add sodium bicarbonate to adjust the alkalinity to 2800, enter the aerobic tank for full aeration, fill the aerobic tank with 30% polyurethane filler, and stay for 17 hours.
[0057] Add 650mg / L of sodium acetate as an external carbon source to the effluent of the aerobic tank, and enter the anoxic tank to react. The anoxic tank is filled with 50% polyur...
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